Method for distillation of sulfur for the preparing radioactive phosphorous nuclide

ABSTRACT

A method for distillation of sulfur for preparing radioactive phosphorous nuclide includes the steps of: charging powdered sulfur into a target tube designed to have an upper and a bottom neck; degassing the target tube to form a vacuum therein, followed by heating the upper neck to seal the target tube; irradiating neutrons into the sealed target tube to produce radioactive phosphorous nuclide; heating the distillation zone to distill the remaining unreacted sulfur; and cleaving the target tube at the bottom neck to separate the distillation and the cooling zone from each other, the separated zones containing the radioactive phosphorous nuclide and the unreacted sulfur, respectively, whereby the radioactive phosphorous nuclide of high purity can be prepared while the sulfur can be recovered at high efficiency.

BACKGROUND OF THE INVENTION

[0001] 1. Field of the Invention

[0002] The present invention relates to a method for distillation of sulfur for the preparing radioactive phosphorous nuclide. More particularly, the present invention relates to an economically favorable and efficient method in which sulfur is converted into radioactive phosphorous nuclide by neutron irradiation while unreacted sulfur is separated from the radioactive phosphorous nuclide by distillation and recovered at high efficiency, with the radioactive phosphorous nuclide remaining high in purity.

[0003] 2. Background of the Related Art

[0004] Emitting β⁻ radiation, nuclides such as ³²P and ³³P find many applications in various fields, including medical treatment, synthesis of labeling compounds, bioengineering experiments, etc.

[0005] The phosphorous nuclide (³²P) can be prepared by the nuclear reaction of ³²S(n,p)³²P or ³¹P(n,γ)³²P. In spite of its guaranteeing very simple chemical treatment after neutron irradiation, the (n,γ) reaction is only adopted in special cases because the uses of the resulting ³²P are limited due to its low specific radioactivity. For use in medical treatment or research experiments, the phosphorous nuclide ³²P is usually obtained by separating it from the sulfur target after ³²S(n,p)³²P nuclear reaction.

[0006] Depending on physical and chemical statuses of the sulfur, separation of the ³²P generally resorts to the following methods.

[0007]³²P may be purified by a wet extraction method in which strong and weak acids are used to extract the phosphorus nuclide from the sulfur target. According to the wet extraction method, ³²P is extracted from finely powdered sulfur irradiated with neutrons in boiling water in the presence of acid [Samsahl, K., Atompraxis 4, 14, 1958; Razbash, A. A. et al., Atomnaya Ehnergiya 70(4), 260, 1991]. In this regard, 2-octanol is used as a wetting agent. This method suffers the following disadvantages. The extraction yield varies with the particle size of the irradiation target sulfur and is significantly decreased when the target is melted or solidified due to the exothermal heat during neutron irradiation. Additionally, the use of acid induces impurities and leaves much solid waste behind, thus completion of the extraction requires additional purification processes.

[0008] Alternatively, ³²P may be prepared by irradiating the sulfate or polysulphide target with neutrons, dissolving the target in water, and then adsorbing or coprecipitating the ³²P thus formed. Because it requires multi-stage processes and produces low recovery yields, this method is scarcely used.

[0009] Suggested as an alternative which can solve the above problems were sulfur distillation methods which are generally classified into: atmospheric distillation in which sulfur is distilled at as high as 500° C. in a nitrogen atmosphere; vacuum distillation in which sulfur is distilled at as low as 180-200° C. under a pressure of 1-10 mmHg [Gharemano, A. R. et al., Radiochemical and Radioanalytical Letters Hungary 58(1), 49, 1983, Ye. A. Karelin et al., Applied Radiation Isotopes 53, 825-827, 2000]. The former employs an inert gas as a carrier in order to reduce the possibility of fire. In the latter method, distillation is carried out at a temperature lower than the ignition point of sulfur by reducing the pressure. These distillation methods are advantageous in that products of high purity can be obtained since no reagents are added upon the separation of phosphorous nuclide from sulfur. However, the methods require facilities such as a vacuum system, a gas-feeding apparatus and a cooling apparatus in order to distill the sulfur irradiated with neutrons in hot cells or glove boxes, as well as require the pressure and temperature to be controlled in relatively narrow ranges. Additionally, where concentrated sulfur is used, it is difficult to recover the whole amount of the highly expensive sulfur, which brings about an economic loss.

[0010] Therefore, there remains a need for an improved method that can prepare phosphorus nuclides of high purity easily and very economically.

SUMMARY OF THE INVENTION

[0011] Leading to the present invention, the intensive and thorough research into the preparation of phosphorus nuclides, conducted by the present inventors in an aim to solve the above problems encountered in prior arts, resulted in the finding that a temperature gradient formed over a target tube irradiated with neutrons allows sulfur to move toward the low temperature site and thus be easily separated from phosphorous nuclide which remains high in purity.

[0012] Thus, it is an object of the present invention to provide a method for safely and efficiently distilling sulfur for preparing radioactive phosphorous nuclide of high purity.

[0013] It is another object of the present invention to provide radioactive phosphorous nuclide with high purity.

[0014] It is still another object of the present invention to provide a method for distilling sulfur using a target tube having thermal profiles.

[0015] Based on the present invention, the above object could be accomplished by a provision of a method for distillation of sulfur for preparing radioactive phosphorous nuclide, comprising the steps of:

[0016] (a) charging powdered sulfur into a distillation zone of a target tube, said target tube being designed to have an upper neck, and a bottom neck which functions as a separation zone, dividing the target tube into a distillation zone and a cooling zone;

[0017] (b) degassing the target tube to form a vacuum therein, followed by heating the upper neck to seal the target tube;

[0018] (c) irradiating neutrons into the sealed target tube to produce radioactive phosphorous nuclide;

[0019] (d) heating the distillation zone to distill the remaining unreacted sulfur, but not the phosphorus nuclide and to allow the gasified sulfur to move over the bottom neck into the cooling zone; and

[0020] (e) cleaving the target tube at the bottom neck to separate the distillation and the cooling zone from each other, the separated zones containing the radioactive phosphorous nuclide and the unreacted sulfur, respectively, whereby the radioactive phosphorous nuclide of high purity can be prepared while the sulfur can be recovered at high efficiency.

[0021] In one embodiment according to the present invention, an apparatus for distilling sulfur for preparing radioactive phosphorous nuclides comprises:

[0022] (a) a distillation heater with heat coils for providing heat to the target tube;

[0023] (b) a heat controller for controlling the heat transferred to the target tube in conjunction with a temperature measurer;

[0024] (c) a tubular vessel for adapting the target tube to the distillation apparatus; and

[0025] (d) a heat insulator for insulating the tubular vessel.

[0026] In one another embodiment according to the present invention, a target tube of the claim designed to have an upper and a bottom neck is used.

[0027] In still another embodiment according to the present invention, the target tube is manufactured by designing to have an upper and a bottom neck; degassing to for a vacuum; and heating to seal the upper neck.

BRIEF DESCRIPTION OF THE DRAWINGS

[0028] The above and other objects, features and other advantages of the present invention will be more clearly understood from the following detailed description taken in conjunction with the accompanying drawings, in which:

[0029]FIG. 1 is a process flow showing the preparation of radioactive phosphorous nuclide by the distillation of sulfur of the present invention;

[0030]FIG. 2 is a schematic view showing the structure of a target tube useful in the present invention, the charging of sulfur in the target tube, and the sealing of the target tube;

[0031]FIG. 3 is a schematic diagram showing the structure of a distillation system useful in the present invention;

[0032]FIG. 4 is a photograph showing the migration of sulfur from a distillation zone to a cooling zone after the distillation of sulfur in the target tubes, which are inserted to lengths of 7 cm (a) and 8 cm (b) into the distillation heater of the distillation system;

[0033]FIG. 5 provides thermal profiles showing a thermal gradient throughout the tubular vessel of the distillation system;

[0034]FIG. 6 is a schematic view showing a procedure of treating the target tube upon and after the distillation of sulfur;

[0035]FIG. 7 is a schematic view showing the division of the target tube into three discrete zones: a distillation zone (a), a separation zone (b), and a cooling zone (c), according to temperatures;

[0036]FIG. 8 is a photograph showing positions of sulfur after sulfur is distilled at 240° C. in a target tube, which is sealed at atmospheric pressure (a) and at 180° C. in a target tube, which is sealed under vacuum and inserted to a length of 7 cm into a distillation tube (b);

[0037]FIG. 9 is a gamma spectrum of H₃ ³²PO₄ Prepared by the distillation method of sulfur in accordance with the present invention; and

[0038]FIG. 10 is a chromatogram obtained after a paper 32 chromatography of H₃ PO₄, which was prepared by the distillation method of sulfur in accordance with the present invention.

DETAILED DESCRIPTION OF THE INVENTION

[0039] It is also to be understood that the terminology employed herein is used for the purpose of describing particular embodiments only and is not intended to be limiting since the scope of the present invention will be limited only by the appended claims and equivalents thereof.

[0040] In describing and claiming the present invention, the following terminology will be used in accordance with the definitions set out below.

[0041] As used herein, ‘sulfur’ means elementary sulfur (³²S), including any forms, without limitation, powder, if need, purified by conventional methods.

[0042] As used herein, a ‘target tube’ means a tubular vessel, without limitation, designed to being able to contain a target material (³²S) with a neck including any sizes.

[0043] As used herein, ‘phosphorous nuclides’ mean ³²P and ³³P prepared by the nuclear reaction of ³²S(n,p)³²P or ³³S (n,p)³³P .

[0044] With reference to FIG. 1, the preparation of radioactive phosphorus nuclides by the distillation of sulfur is briefly described in a process flow diagram, according to the present invention. As seen, the preparation of radioactive phosphorus nuclides starts with the charging of sulfur into a target tube designed to have an upper and a bottom neck. In this regard, the weight of the mixture must be controlled relative to the dose of neutron radiation to be emitted. Then, the tube is degassed to form a vacuum. The upper neck is heated to seal the target tube, followed by placing the vacuum-sealed target tube in a shielded environment. Subsequently, neutrons are irradiated to the charged sulfur to cause a nuclear reaction. Using a distilling apparatus, unreacted sulfur, except for phosphorus nuclides, is transferred into a cooling zone. Afterwards, the target tube is cleaved at the bottom neck to recover unreacted sulfur and the phosphorous nuclide thus formed, separately. The recovered phosphorus nuclide is purified to higher homogeneity by a process including an acid treatment.

[0045] With reference to FIG. 2, there is shown a target tube 10 useful in the present invention, which is in an open state, and, after being charged with sulfur 100, in a sealed state. As seen in the schematic diagrams of FIG. 2, the target tube 10 in an open state is structured to have an upper neck 11 and a bottom neck 12 and divides into three parts (10 a, 10 b and 10 c). After being charged with powdered sulfur 100, the target tube 10 is degassed with the aid of a vacuum machine, to form a vacuum therein. Heating the upper neck 11 with a torch then seals the target tube 10 (10 a+10 b).

[0046] In order to irradiate neutrons into the sulfur 100, the sealed target tube 10 is placed in a shielded environment. The irradiation of neutrons converts the sulfur 100 into a phosphorus nuclide 300. The shielded environment may consist of a general shielding apparatus well known in the art. Upon neutron irradiation, a ³²S(n,p)³²P nuclear reaction (or ³³S (n,p)³³P nuclear reaction) is caused to produce ³²P 300 (or ³³P) which exists, together with the unreacted sulfur 10 a, in a distillation zone of the target tube 10.

[0047] Most of the non-sublimate materials remaining after the neutron irradiation behave like phosphorus nuclides 300, so that the sulfur powder 100, used as the target, must be of high purity. That is, sulfur 100 for use in the present invention must be in a concentrated form or must be purified to high homogeneity. Depending on the vacuum machine used, the pressure of the sealed, vacuum target tube 10 preferably falls within the range of about 0.1 to 0.01 torr.

[0048] By heating, the upper neck 11, as described above, is melted to seal the target tube 10, while the bottom neck 12 functions to prevent the countercurrent of the unreacted sulfur 100 a from the cooling zone upon distillation of said unreacted sulfur 100 a.

[0049] The target tube 10 used in the present invention is not particularly limited if it can transmit the neutron radiation to convert sulfur 100 into phosphorus nuclides 300, and is preferably made of hard glass. Most preferable is a quartz tube. It is obvious to those skilled in the art that the size of the target tube 10 and the position and height of the necks 11, 12 can be adjusted depending on the neutron irradiator and the content of the sulfur 100.

[0050] After completion of the neutron irradiation, the target tube 10 is mounted onto a distillation apparatus 200 in which the unreacted sulfur 100 a mixed with the phosphorus nuclide 300 is moved over the bottom neck 12 into the opposite zone within the target tube 10. Referring to FIG. 3, there is shown a distillation apparatus 200 useful in the present invention, in which the target tube 10 is mounted. The distillation apparatus 200 comprises a distillation heater 201 with a heat coils 201 b for providing heat to the target tube 10, a heat controller 203, for controlling the heat transferred to the target tube 10, in conjunction with a temperature measurer 202 with a temperature probe 202 a, a tubular vessel 201 a for adapting the target tube 10 to the distillation apparatus 200 and a heat insulator 201 c. In order to receive the target tube 10, the tubular vessel 201 a with a conductor i.e, metal is designed to have an open side and an inner diameter larger than the outer diameter of the target tube 10.

[0051] To adapt the target tube 10 to the distillation heater 201, the distillation zone containing a mixture of the unreacted sulfur 100 a and the nuclear reaction product phosphorus nuclide 300 is fitted into the closed portion of the tubular vessel 201 a, while the cooling zone for recovering the unreacted sulfur 100 a is positioned in the open position.

[0052] After being distilled by the heat provided from the heater 202, the unreacted sulfur 100 a moves to the cooling zone positioned in the open portion of the tubular vessel 201 a, and is air-cooled therein.

[0053] The position of the tubular vessel 201 a relative to the target tube 10 mounted into the distillation apparatus 200 is found to have a great influence on the distillation time and yield. In order to examine the effect of the position of the target tube 10 on the separation of sulfur 100, distillation was carried out at 180° C. at 0.1 torr in target tubes 10 inserted in the tubular vessel 201 a to different lengths. With reference to FIG. 4, there are shown the results obtained from the target tubes inserted 7 cm (a) and 8 cm (b) into the tubular vessel 201 a. As can be seen, when a greater length of the target tube is inserted, the sulfur is moved to and condensed at a site of the cooling zone (10 b), which is more distant from the distillation zone. The results show that, when the temperature distribution inside the target tube 10 is not uniform, but forms a gradient such that the temperature is higher than 180° C. at the distillation zone and lower than 180° C. at the cooling zone, the unreacted sulfur 100 a readily moves from the distillation to the cooling zone. Additionally, like the neck of the target tube 10, a physical barrier (separation zone) must be provided between the distillation zone and the cooling zone. This physical barrier plays an important role in separating the unreacted sulfur 100 a from the product phosphorus nuclide 300. Because the unreacted sulfur 100 a is cooled at lower than 160° C. into a liquid phase in the cooling zone and has an increased viscosity, there is the possibility that the unreacted sulfur 100 a might move backwardly into the distillation zone. However, although the unreacted sulfur 100 a moves leftward form the start point of the cooling zone as shown in FIGS. 4a and 4 b, the countercurrent into the distillation did not occur due to the presence of the neck in the target tube 10.

[0054] A detailed description will be given of the distillation process of the present invention, below.

[0055] Heating the target tube 10 in the distillation apparatus 200 gasifies the sulfur 100. All the gas moves into the cooling zone, whereas the product ³²P 300 still remains attached to the inner wall of the target tube 10 within the distillation zone. When the distillation zone of the target tube 10 is heated at 160-240° C., the unreacted sulfur 100 a, except for the produced phosphorus nuclide 300, is distilled in the distillation zone and condensed in the cooling zone. The distillation temperature is preferably on the order of 180 to 220° C. This distillation temperature is high enough to distill the sulfur, considering the distillation point of sulfur 100 and that the inner pressure of the target tube 10 ranges from 0.1 to 1 torr. Preferably, the distillation is carried out at 180° C. when the inner pressure of the target tube 10 is 0.1 torr. For example, at a temperature below the lower limit of the distillation range, the sulfur 100 is not sufficiently distilled and is difficult to recover in its entirety, resulting in economic loss.

[0056] The time it takes to distill the sulfur 100 is dependent on the quantity of the sulfur 100 in the target tube 10. According to embodiments of the invention, it was found that it takes approximately 1.5-2 hours to completely distill 1 g of sulfur powder 100 at 180° C. at 0.1 torr in a target tube 10 with a dimension of 1.1×12 cm (outer diameter×length).

[0057] Once gasified, the sulfur 100 a moves over the physical barrier, that is, the neck 12 (separation zone), into the cooling zone and then is condensed to solidify. In the cooling zone, the unreacted sulfur 100 a is increased in viscosity and condensed into a liquid phase, which might move backwardly into the distillation. In the target tube 10, the bottom neck 12, as demonstrated in FIGS. 4a and 4 b, prevents the countercurrent.

[0058] The target tube 10 may be divided into three zones: distillation (a), separation (b) and cooling zones (c). There is a temperature gradient throughout from the distillation zone to the cooling zone upon distillation, as depicted in FIG. 5. According to the temperature profiles of FIG. 5, a temperature gradient from approximately 180 to 200° C. is formed over the distillation and cooling zones, allowing the gasified sulfur to be effectively recovered in a powder form. The cooling of the target tube 10 may resort to an external cooling water feeder, although this be sufficiently accomplished by allowing the target tube 10 to remain in contact with external air at room temperature.

[0059] Finally, to recover the ³²P 300 (or ³³P) and the unreacted sulfur 100 a, the target tube 10 is cleaved, followed by a suitable chemical treatment. The unreacted sulfur 100 a may be reused without further treatment.

[0060] The ³²P 300 (or ³³P) remaining in the target tube 10 is leached by the addition of acid, and the leachate is purified to afford a highly pure radioactive isotope at a high purity. The purification may be carried in a conventional manner, and preferably by chromatography.

[0061] After the cleavage of the target tube 10, the tube fragment 10 b containing the unreacted sulfur 100 a may be joined to a remaining portion by use of a torch to give a fresh target tube 10 useful in the present invention.

[0062] In accordance with the present invention, the movement of the unreacted sulfur 100 a is found not to occur when the target tube 10 is not vacuumed by degassing. By contrast, all of the unreacted sulfur 100 a moves into the cooling zone in the presence of a temperature gradient over the vacuum target tube 10, which leads to the unreacted sulfur 100 a recovery yield of 99.9% or higher.

[0063] Therefore, without requiring complex distillation apparatuses 200 and vacuum and cooling systems, the distillation method of the present invention is very simple in comparison to conventional distillation methods, as well as being able to easily distill sulfur in the presence of a temperature gradient which is formed from the distillation to the cooling zone according to the vacuum level of the target tube 10. Additionally, the method of the present invention can be industrially utilized because it can be easily scaled up for the mass production of phosphorous nuclides 300.

[0064] The phosphorous nuclides (³²P) 300 prepared in accordance with the present invention is found to show a nuclide purity of 99% or higher and a radiochemical purity of 99% or higher, with a solid content of 0.2 mg/ml or less. Highly pure phosphorous nuclides (³²P) 300 has many applications in various industries, including radiotherapy, synthesis of radioactive labeling compounds, bioengineering research, etc.

[0065] Having generally described this invention, a further understanding can be obtained by reference to certain specific examples, which are provided herein for purposes of illustration only and are not intended to be limiting unless otherwise specified.

EXAMPLE 1 1. Purification of Sulfur

[0066] Powdered sulfur (Merck Art 7892) was charged into a subliming reactor, followed by heating at 150□ to melt the sulfur. The subliming reactor was connected with a vaporizing apparatus, reduced pressure to 100 mm of Hg and then heated to at 300□. The sublimed sulfur was moved to and condensed at receiving flask to obtain an yellowish pure sulfur. The highly pure sulfur was prepared repeatedly three times in this procedure, and the purity (99.99%) was determined by NMR detection.

2. Degassing and Distillation

[0067] The sulfur purified in the above step 1) was ground and charged into a target tube, which was made of quartz in a variety of sizes (see Table 1). After being charge with sulfur, the target tube was degassed with the aid of a vacuum machine to form a vacuum state. The target tube was then sealed by heating with a torch, as described in the procedure of FIG. 2. After sealed target tube was placed in a distillation apparatus, distilling was carried out until the sulfur could no longer be seen in the distilling zone. The conditions of inner pressure and temperature of target tube are as follows. TABLE 1 amount target tube inner of dimensions Temper- pressure of distilling sulfur (diameter × ature target tube time No. (g) length) (□) (torr) (hours) 1 0.5 1.1 cm × 7.3 cm 180 0.1 1 2 1 1.1 cm × 12 cm 240 atmospheric — 3 1 1.1 cm × 12 cm 180 0.1 2.3 4 1 1.1 cm × 12 cm 180 0.1 2.2 5 1 1.1 cm × 12 cm 220 0.1 1.5 6 1 1.1 cm × 12 cm 240 0.1 1.2 7 3 2.6 cm × 7.3 cm 240 0.1 3

EXPERIMENTAL EXAMPLE 1 1. Recovery Yield of Sulfur

[0068] To determine yield of the sulfur distilled followed by recovering in the above Example 1, the amount of sulfur in the cooling zone of the each target tube was weighed using a precision balance. As a result, it was confirmed that the each yield of sulfur recovered in item Nos. 1-7 of Table 1 was over 99.9%.

2. Effect on Distilling Temperature

[0069] To determine effect on distilling temperature, the distillation of sulfur carried out as follows.

[0070] After the insertion of a probe into a glass rod of the same size as the target tube (FIG. 3), the probe was heated to various temperatures, i.e., 80V (145□), 82V (160□), 85V (180□), 90V, (210□), using a slighdax as a temperature-controller. The variation of temperature at each voltage was detected at intervals of 1 cm relative to the total length of the target tube, thus obtaining the result shown in FIGS. 5 and 7. FIG. 5, in particular, shows the thermal gradient throughout the tubular vessel of the distillation system at each voltage, and FIG. 7 illustrates the division of the target tube into three discrete zones. As shown in FIGS. 5 and 7, the target tube has a thermal profile (or temperature gradient) in which the inner temperature of the target tube degrades gradually, divides into each fractional zone—(a) a distillation zone; (b) a separation zone; and (c) a cooling zone according to its inner temperature. Concretely, since the difference between (a) distilling zone and (c) condensing zone is about 180˜200□, it may be preferably possible to control the distillation of sulfur using the target tube designed to in accordance with the present invention.

3. Effect on Inner Pressure of the Target Tube

[0071] To determine effect on inner pressure of the target tube, the distillation of sulfur in a variety of inner pressure and its temperature carried out as follows.

[0072]FIGS. 8A and 8B show two-type target tubes as the positions of sulfur after sulfur was distilled at 240 □ in a target tube, which was sealed at atmospheric pressure (FIG. 8A) and at 210□ in a target tube that was sealed under 0.1 torr and inserted into a length of 7 cm into a distillation tube (FIG. 8B). As shown in FIG. 8A, it is found that the molten sulfur does not move to the cooling zone (c), wholly remaining in the distillation zone (a). On the contrary, FIG. 8B shows that total amount of the molten sulfur is move to the cooling zone. This is evidence that it can be more effective to distill sulfur when the target tube is degassed and sealed.

EXAMPLE 2 1. Preparation of Radioactive Phosphorous (³²P)

[0073] Radioactive phosphorous was prepared according to the method of the present invention.

[0074] Five grams of elementary sulfur (powder) was charged into a target tube having a dimension of 1.1 cm×12 cm (diameter×length). The tube was degassed with the aid of vacuum machine to reach an inner pressure of 0.1 torr, and then sealed by heating with a torch. To irradiate radical rays, the target tube was inserted into an aluminum capsule immersed in a bath of cooling water. After cooling down, the aluminum capsule was sealed by cold rolling and transferred to the irradiation reactor.

[0075] The sealed capsule was inserted into an irradiation reactor (IP No. 15) in a HANARO reactor (kept by the inventor) for producing an isotope and then was irradiated radical rays for 72 hours. The fast neutron flux of irradiation hole was 2.38×10¹² n/cm²s. The used sulfur is highly purified in the same procedure as described in Example 1 (purity >99%).

[0076] After the completion of irradiating, the target tube isolated from the aluminum capsule was inserted into the distillation apparatus, heated to maintain the temperature around the neck to 180□ under regulated voltage and then distilled for one hour. As the distillation of sulfur was progressed, the yellowish powdery sulfur was observed the in cooling zone. After the completion of distillation, the powdery sulfur was present in the cooling zone. In contrast, any phosphorous nuclides (³²P) in the distilling zone were not observed.

[0077] After the target was cleaved at its neck to recover phosphorous nuclides (³²P) and unreacted sulfur thus formed, separately, the sulfur in the half-target tube (of cooling zone) was charged into a storage that was previously weighed.

[0078] To recover the obtained phosphorous nuclides, a chemical treatment carried out as follows.

[0079] A mixture of 20 ml of 0.1N HCl and 0.1 ml of 30% H₂O₂ aqueous solution was added to the half-target tube (with ³²P present) and the remaining ³²P was leached out at 70□ for two hours.

[0080] A form of orthophosphoric acid (H₃ ³²PO₄) dissolved in the HCl aqueous solution was present in the obtained leachate. To delete the radiated cation in the leachate, purification of the leachate carried out using column chromatography. After a cation exchange resin (Bio Rad AG50W-X8H⁺, 100-200 mesh) was poured into a water to fully swell, thus the swelled resin was filled with column (Bio Rad Chromatography Column, 0.8×4 cm) in a volume of 2 ml and then washed with 2 ml of 0.05M HCl aqueous solution. Passing the leachate through the column, H₃ ³²PO₄ solution was recovered. In order to obtain further H₃ ³²PO₄ remaining in the column, 2 ml of 0.05M HCl aqueous solution was past through the column, repeatedly twice in this procedure. The obtained mixture was combined with the earlier recovered H₃ ³²PO₄ solution.

[0081] In addition, H₃ ³²PO₄ was prepared in the same manner as the above procedure except for cooling time (5.7 days).

EXPERIMENTAL EXAMPLE 2 1. Test for Radionuclidic Purity

[0082] Because ³²P is a pure beta radiator, the identification of the obtained ³²P solution was accomplished by a measurement of its half-life.

[0083] Five milliliters of H₃ ³²PO₄ solution charged into an ample (volume 10 ml, thickness 0.6 mm) was inserted into ionization chamber (Capintec “127-R”), which was previously calibrated using a standard source and then measured for its radioactivity using a beta counter (Capintec “beta eta C”).

[0084] To detect impurities, the vial with a volume of 10 ml containing a small portion of H₃ ³²PO₄ solution was inserted into a plastic box having a thickness of 3 cm to shield Bremsstrahlung radiation radiated from the ³²P. A gamma radiation spectrum was recorded using a multiple-channel analyzer equipped with an HPGe detector. The results are summarized in Table 2 and in FIG. 9. TABLE 2 Amount Radioactivity of ³²P of Irradiation Cooling Calcu- No. sulfur time* time observed lated** Yield 1 5 g 72 hours 25.7 days 1.42 mCi 1.45 mCi 97.9% 2 5 g 72 hours  5.7 days 3.65 mCi 3.83 mCi 95.3%

[0085] As shown in Table 2, it was confirmed that ³²P prepared according to the method of the present invention was highly pure, since the yield of ³²P was over 95% relative to that of the calculated value.

[0086] In addition, in FIG. 9, gamma-radiation impurities were detected at the lowest limit of 5×10⁻⁵% and not exceeding 0.001%. In FIG. 9, K-40 (1460 KeV) and Tl-208 (2614 KeV) are means a background radiation.

2. Test for Radiochemical Purity

[0087] To determine radiochemical purity of ³²P prepared in Table 2 (item No. 2), paper chromatography was carried out as follows.

[0088] Since the leachate, ³²P dissolved in 0.1N HCl, is present as a form of H₃ ³²PO₄, the inventors carried out a paper chromatography to identify the radiochemical purity of ³²P. As a stationary phase, Whatman paper No. 1 was used before the paper washed with diluted HCl aqueous solution followed by air-drying. As a mobile phase, the mixture of isopanol, H₂O, trichloro acetic acid, and ammonia (in quantities of 75 ml, 25 ml, 5 g, and 0.3 ml, respectively) was used. On the paper was pointed one drop of the mixture, dried, and then developed for two hours. Using a beta chromatogram scanner, the Rf value was measured, and the thus obtained chromatogram is show in FIG. 10.

[0089]FIG. 10 shows that the radiochemical purity of H₃ ³²PO₄ was over 99% and impurities remained in small quantities. Although FIG. 10 does not show compositions of the impurities, the presence of orthophophate (Rf value: 0.76), metaphosphate (Rf value: 0.00), and pyrophosphate (Rf value: 0.40) was observed. This result is evidence that the ³²P prepared according to method of the present invention is highly pure.

3. Test for Solid Content

[0090] To determine an amount of ³²P obtained according to the present invention, a content of solid in the leachate was detected as follows.

[0091] The H₃ ³²PO₄ leachate was poured into a vial (1 ml, 0.15 mCi), which was previously weighed, and a solute was removed by evaporation under infrared lamp, and then the amount of the obtained solid was weighed (content: 0.2 mg/ml).

[0092] The characteristics of the ³²P prepared according to method of the invention, therefore, are as follows: properties Results Radiochemical H₃ ³²PO₄ in diluted HCl form Radioactive 1.11 to 2.96 GBq (30˜80 mCi) /ml concentration Radiochemical Orthophosphate content >95% purity Radionuclide >99%, no extraneous gamma purity impurities Noticeable solid content <0.2 mg/ml Appearance clear colorless solution, turns the glass vial brown

[0093] Hence, the method according to the present invention is suitable for preparation of ³²P and ³³P with about 100 mCi of radioactive concentration using costly and highly concentrated ³²S. Especially, it is fully possible to prepare 1˜2 Ci of ³²P and ³³P, when 2˜3 g of ³²S as a target material is used, by irradiating followed by chemical treatment.

[0094] Moreover, the obtained H₃ ³²PO₄ is preferably used for preparing ³²P labeled nucleotides as well as bone pain palliation in metastasis.

[0095] As herein above described and exemplified, the method in accordance with the present invention is practicable for a preparation method for radioactive phosphorous, which comprises inserting powdery sulfur into a target tube with neck, irradiating the powdery sulfur to convert radioactive phosphorous, and distilling the target tube with thermal profile followed by recovery. In addition, the method of the invention enables the effective preparation of radioactive phosphorous with high purity and safety. The method also enables recovery as almost total contents of the used sulfur, as it was, and reusing the used target tube subsequently so that can be directly drop in another preparation of ³²P.

[0096] The embodiments are merely exemplary and are not to be construed as limiting the present invention. The present teachings can be readily applied to other types of apparatuses. The description of the present invention is intended to be illustrative, and not to limit the scope of the claims. Many alternatives, modifications, and variations will be apparent to those skilled in the art. 

What is claimed is:
 1. A method for distilling sulfur for preparing radioactive phosphorous nuclide, comprising the steps of: (a) charging powdered sulfur into a distillation zone of a target tube, said target tube being designed to have an upper neck, and a bottom neck which functions as a separation zone, dividing the target tube into a distillation zone and a cooling zone; (b) degassing the target tube to form a vacuum therein, followed by heating the upper neck to seal the target tube; (c) irradiating neutrons into the sealed target tube to produce radioactive phosphorous nuclide; (d) heating the distillation zone to distill the remaining unreacted sulfur, but not the phosphorus nuclide and to allow the gasified sulfur to move over the bottom neck into the cooling zone; and (e) cleaving the target tube at the bottom neck to separate the distillation and the cooling zone from each other, the separated zones containing the radioactive phosphorous nuclide and the unreacted sulfur, respectively.
 2. The method of the claim 1, wherein the heating in the step d) is carried out at a temperature ranging from 160□ to 240□.
 3. The method of the claim 1, wherein the heating in the step d) is carried out at a temperature ranging from 180□ to 220□.
 4. The method of the claim 1, wherein after degassing in the step b), the inner pressure of the target tube ranges from 0.1 torr to 1 torr.
 5. The method of the claim 1, wherein the depth of the bottom neck of the target tube is controlled relative to an amount of powdered sulfur to prevent the countercurrent of the sulfur from the cooling zone upon distillation of said sulfur.
 6. The method of the claim 1, wherein the thus obtained radioactive phosphorous nuclides in the step e) is recovered by chemical treatment.
 7. The method of the claim 6, wherein the chemical treatment comprises; extracting the radioactive phosphorous nuclides with acid solution to form H₃ ³²PO₄ followed by passing thus obtained mixture through column chromatography.
 8. The method of the claim 1, wherein the unreacted sulfur in the step e) is able to reuse another preparation of radioactive phosphorous nuclides.
 9. The method of the claim 1, wherein the cooling of unreacted sulfur in the step e) is carried out under air-cooling or by cooling water.
 10. An apparatus for distilling sulfur for preparing radioactive phosphorous nuclides of the claim 1 comprising: (a) a distillation heater with heat coils for providing heat to the target tube; (b) a heat controller for controlling the heat transferred to the target tube in conjunction with a temperature measurer; (c) a tubular vessel for adapting the target tube to the distillation apparatus; and (d) a heat insulator for insulating the tubular vessel.
 11. The apparatus of the claim 10, wherein the tubular vessel is designed to have an open side and an inner diameter larger than the outer diameter of the target tube.
 12. The apparatus of the claim 10, wherein the cooling zone for recovering the unreacted sulfur is positioned in the open portion of the tubular vessel.
 13. A target tube of the claim 1 designed to have an upper and a bottom neck.
 14. A method for manufacturing useful the target tube of the claim 1 comprises designing to have an upper and a bottom neck; degassing to for a vacuum; and heating to seal the upper neck. 